BW Shipping. GAS FORM-C based on the OCIMF / SIGTTO SHIP INFORMATION QUESTIONNAIRE for GAS CARRIERS 2nd Edition 1998

Transcription

1 BW Shipping GAS FORM-C based on the OCIMF / SIGTTO SHIP INFORMATION QUESTIONNAIRE for GAS CARRIERS 2nd Edition 1998 Specifications of the vessel and the gas installations are believed to be correct as per design specifications and capacities, but not guaranteed, and consequently Owners are not to be held accountable for such. We further reserve our rights for normal wear and tear on cargo equipment in respect of loading-, discharging-, cooling-rates and time for changing cargo grades etc., including but not limited to capacity of cargo re-heaters, compressors, pumps and other equipment, as described in this form-c as these descriptions, as described above, refers to design capacities. Page 0

2 INDEX GENERAL INFORMATION PAGE A1 Principal Ship Particulars 2-3 A2 Hull Dimensions 4 A3 Immersion 4 A4 Loaded Particulars 4-5 A5 Parallel Mid-Body Dimensions 6 A6 Bunker Specifications and Capacities 6 A7 Fuel Consumption Details 6 A7 Speed/Consumption (Appendix) 7 A8 Main Engine Particulars 7 A9 Auxiliary Plants 7 A10 Power/Speed Information 7 A11 Thrusters 7 A12 Fresh Water 7 A13 Ballast Capacities and Pumps 8 A14 Mooring Equipment 8-10 A15 Navigational Equipment A16 Communication and Electronics 11 CARGO SYSTEMS B1 Cargo - General Information 12 B2 Cargo Tanks 12 B3 Cargo Tank Capacities B16 Deck Tank Capacities B4 Loading Rates B5 Discharging - General B6 Discharge Performance 18 B7 Unpumpables 18 B8 Vaporising Unpumpables 18 B9 Reliquefaction Plant B10 Section not in use. B11 Cargo Temperature Lowering Capability 19 B12 Inert Gas and Nitrogen B13 Cargo Tank Inerting / De-Inerting 20 B14 Gas Freeing to Fresh Air 20 B15 Changing Cargo Grades B17 Pre-Loading Cooldown B18 Vaporiser 22 B19 Blower 22 B20 Cargo Re-Heater 22 B21 Hydrate Control 22 B22 Cargo Measurement B23 Cargo Sampling 23 B24 Cargo Manifold B25 Cargo Manifold Reducers B26 Connections to Shore for ESD and Communication Systems 26 B27 Manifold Derrick/Crane 26 B28 Stores Derrick/Crane B29 Sister Vessel(s) Page 1

3 SECTION A GENERAL INFORMATION A1 PRINCIPAL SHIP PARTICULARS 1.1 Date questionnaire completed 25-Apr Name of vessel BW BALDER 1.3 LR/IMO number Last previous name AURORA BALDER Date of name change 24/04/ Second last previous name Date of name change 1.6 Third last previous name Date of name change Fourth last previous name Date of name change Flag Marshall Islands 1.9 Port of Registry Majuro 1.10 Official number Call sign V7CB INMARSAT FBB numbers Vessel's telephone number (V-Sat) Vessel's mobile number 1.14 Vessel's fax number Vessel s telex number (Inmarsat-C) Vessel's address bwbalder@ship-bw.wilhelmsen.com INMARSAT C number Vessel's MMSI number Type of vessel Gas carrier (VLGC) OWNERSHIP AND OPERATION 1.20 Registered Owner BW Constellation II Limited Full address Clarendon House 2 Church Street Ham Bermuda Office telephone number Office telex number Office fax number Office address Contact person Contact person after hours telephone number (65) (65) lpg.commercialdevelop@bwlpg.com Joel Wee (65) Name of technical operator (If different from above) Wilhelmsen Ship Management Sdn Bhd Full Address 18th floor, 1 Sentral, Jln Travers, Kuala Lumpur Sentral, Kuala Lumpur, Malaysia. Office telephone number /5601 Office telex number NIL Office fax number / 5605 Office address wsmkl.vetting@wilhelmsen.com Contact person Mr. Peter Vekemans Contact person after hours telephone number Emergency callout number Emergency callout pager number Contact details for person responsible for oil spill response Glen Motha (General Manager), Number of years controlled by technical operator 1.1 Years Page 2

4 1.22 Total number of ships operated by this Operator Number of years ship owned 1.1 Years Name of commercial operator (If different from above) BW LPG Ltd Full Address Maple Tree Business City, 10 Pasir Panjang Rd, #17-02 Singapore Office telephone number / Office telex number Office fax number Office address fleetops2@bwlpg.com Contact person Capt. Kevin Knott Contact person after hours telephone number Emergency callout number Emergency callout pager number Number of years controlled by commercial operator 0.3 Years BUILDER 1.24 Builder Hyundai Heavy Industries 1.25 Name of yard vessel built at HHI 1.26 Hull number Date keel laid 14-Sep Date launched 18-Dec Date delivered 14-Mar Date of completion of major hull changes, - if any If changes were made, what changes were made and at which yard were they carried out NA CLASSIFICATION 1.32 Classification society Det Norske Veritas 1.33 Class Notation +1A1 Tanker for liquefied Gas Ship Type 2G (- 50C, 610kg/m3,0.275 bar), E0, BIS,TMON,COAT-PSPC(B), BWM(T), SPM, CLEAN, NAUTICUS(New building), ERS 1.34 If Classification society changed, name of previous society N/A 1.35 If Classification society changed, date of change N/A 1.36 Was ship built in accordance with the following regulations: IMO N/A US COAST GUARD N/A RINA Other: 1.37 IMO certification Certificate of fitness - IGC DNV.GL Certificate - A328 NA Certificate - A329 NA Letter of Compliance NA Issued by NA 1.38 Unattended Machinery Space Certificate DNV.GL 1.39 Net Registered Tonnage Gross Registered Tonnage Suez Net Tonnage - Canal Tonnage Suez Gross Tonnage Panama Net Tonnage - Canal Tonnage Panama Gross Tonnage - Page 3

5 A2 HULL DIMENSIONS 2.1 Length overall (LOA) Metres 2.2 Length between perpendiculars (LBP) Metres 2.3 Distance bow to bridge Metres 2.4 Distance bridge front - mid point manifold Metres 2.5 Distance bow to mid-point manifold Metres 2.6 Extreme breadth Metres 2.7 Extreme depth Metres 2.8 Summer draught Metres 2.9 Corresponding Summer deadweight Light displacement Loaded displacement (Summer deadweight) Cargo tanks cubic capacity - 100% Cubic metres Deck tank(s) cubic capacity - 100% N/A Cubic metres Cargo tanks cubic capacity - 99% Cubic metres Deck tank(s) cubic capacity - 99% N/A Cubic metres 2.13 Distance from keel to highest point Metres 2.14 Air draught (normal ballast condition) Metres A3 IMMERSION / metres draught 3.1 TPC - in normal ballast condition TPC - in loaded condition (summer deadweight) A4 LOADED PARTICULARS 4.1 Cargo grade n-butane iso-butane 4.2 Density Cargo loadable Bunkers - FO Bunkers - DO Fresh water Stores & spares 4.8 Lub oil Ballast x Draught - forward Metres Draught - aft Metres Draught - mean Metres Cargo grade Propane Propylene Density Cargo loadable Bunkers - FO Bunkers - DO Fresh water Stores & spares Lub oil Ballast 0 0 Deadweight Draught - forward Metres Draught - aft Metres Draught - mean Metres Page 4

6 Cargo grade Ethylene Ammonia Density NA NA Cargo loadable Bunkers - FO Bunkers - DO Fresh water Stores & spares Lub oil Ballast Deadweight Draught - forward Draught - aft Draught - mean Cargo grade VCM Propylene Oxide Density NA NA Cargo loadable Bunkers - FO Bunkers - DO Fresh water Stores & spares Lub oil Ballast Deadweight Draught - forward Draught - aft Draught - mean Metres Metres Metres Metres Metres Metres Page 5

7 A5 PARALLEL MID-BODY DIMENSIONS Load Draft Ballast Draft Light Ship C/L 5.1 Light ship Metres 5.2 Forward to mid-point manifold - light ship Metres 5.3 Aft to mid-point manifold - light ship Metres 5.4 Normal ballast Metres 5.5 Forward to mid-point manifold - normal ballast Metres 5.6 Aft to mid-point manifold - normal ballast Metres 5.7 Loaded SDWT Metres 5.8 Forward to mid-point manifold - loaded SDWT Metres 5.9 Aft to mid-point manifold - loaded SDWT Metres A6 BUNKER CAPACITIES Grade 98% Main engine 380cST 2695 Auxiliary engine(s) MGO 632 Other: A7 FUEL CONSUMPTION DETAILS 7.1 At sea - normal service speed Fuel oil /day Diesel oil /day Gas oil /day 7.2 At sea - normal service speed - while conditioning cargo Fuel oil /day (Cooling down condition) Diesel oil /day Gas oil /day 7.3 In port - loading Fuel oil /day Diesel oil /day Gas oil /day 7.4 In port - discharging Fuel oil /day Diesel oil /day Gas oil /day 7.5 In port - idle Fuel oil /day Diesel oil /day Gas oil /day Based on FO LCV=10200kcal/kg, MDO LCV=10200kcal/kg under ISO reference condition Grade Page 6

8 A7 SPEED/CONSUMPTION Copies of the vessel's Speed and Consumption Graph for both Laden and Ballast conditions are enclosed? NO A8 MAIN ENGINE PARTICULARS 8.1 Main engine make and type HYUNDAI- MAN B&W / 6G60ME-C Number of units Maximum continuous rating (MCR) per engine RPM kw Total available power at 103 rpm 8.5 Normal service power at 89 rpm kw A9 AUXILIARY PLANTS 9.1 Make and type of auxiliary generators / engines HHI-EMD / 8H21/ Number of units Maximum generator output per unit RPM Kilowatts Unit no Unit no Unit no Shaft generator Total available power Emergency generator Emergency fire pump - type CENTRIFUGAL, VERTICAL, SELF-PRIMING, ELEC. MOTOR Delivery pressure 10 Bar Motive power Electric If electrical, - indicate power required 55 Kilowatts 9.8 Steering gear - type Indicate power required to steer the vessel with one pump 2-RAM 4 Cylinder Electro Hydraulic unit 45 Kilowatts A10 POWER/SPEED INFORMATION 10.1 Trial data BHP MRC SHP Speed Knots Draught 6.61 Metres 10.2 Normal service speed BHP MRC SHP Speed Knots Draught 6.64 Metres A11 THRUSTERS 11.1 Make and type N/A 11.2 Bow thruster (output) N/A Kilowatts 11.3 Stern thruster (output) N/A Kilowatts A12 FRESH WATER 12.1 Capacity of distilled tanks 12.2 Capacity of domestic tanks Daily consumption Distilled Domestic Daily evaporator capacity 22 Page 7

9 A13 BALLAST CAPACITIES AND PUMPS Tank Capacity (m3) Number 13.1 Fore peak Wing and or side tanks 13.3 Double bottom tanks Aft peak Other: 13.6 Total Ballast pump make and type SHIN SHIN MACH./ MDC 350C 13.8 Number of pumps Total capacity 1600 (2 x 800) M3/hour Location E/R FLOOR FWD Control location CARGO CONTROL ROOM A14 MOORING EQUIPMENT 14.1 ROPES Indicate on the diagram below the position of: Winch Mounted Ropes (R) Open Fairleads (O) Closed Fairleads (C) Alternatively enclosed copy of vessel's Mooring arrangements in A4 format. NO C 3 x C 3 x C 2 x R 2 x R 3 x C 2 x R 3 x C 3 x C 3 x C 4 x C 2 x R 2 x R 3 x C 3 x C 4 x C 2 x R 2 x R 3 x C 2 x R 3 x C C MOORING ROPES (ON DRUMS) Mooring Ropes (On Drums) Forecastle - Number 6 Diameter 35 mm. Material Length GALV STEEL WIRE ROPE(IWRC) 220 Metres Breaking Strength 837 KN Mooring Ropes (On Drums) Forward Main Deck - Number 2 Diameter 35 mm. Material Length GALV STEEL WIRE ROPE(IWRC) 220 Metres Breaking Strength 837 KN Page 8

10 Mooring Ropes (On Drums) Aft Main Deck - Number 2 Diameter 35 mm. Material Length GALV STEEL WIRE ROPE(IWRC) 220 Metres Breaking Strength 837 KN Mooring Ropes (On Drums) Poop - Number 6 Diameter 35 mm. Material Length GALV STEEL WIRE ROPE(IWRC) 220 Metres Breaking Strength 837 KN OTHER MOORING LINES Mooring Ropes not on Drums - Number 12 Diameter 62 mm. Material Length Polyolefin resin & Polyester Mixed 220 Metres Breaking Strength 829 KN Fire Wires - Number 2 Diameter 38 mm. Material Length GALV STEEL WIRE ROPE (IWRC) 130 Metres Breaking Strength 539 KN 14.2 MOORING WINCHES Forecastle - Number 2 Single Drum or Double Drums DOUBLE DRUM Split Drums Y/N Y Motive Power HYD. Heaving Power 20 Brake Capacity 50.4 Hauling Speed 15 Metres/Min. Forward Main Deck - Number 2 Single Drum or Double Drums DOUBLE DRUM Split Drums Y/N Y Motive Power HYD. Heaving Power 20 Brake Capacity 50.4 Hauling Speed 15 Metres/Min. Aft Main Deck - Number 1 Single Drum or Double Drums DOUBLE DRUM Split Drums Y/N Y Motive Power HYD. Heaving Power 20 Brake Capacity 50.4 Hauling Speed 15 Metres/Min. Poop - Number 3 Single Drum or Double Drums DOUBLE DRUM Split Drums Y/N Y Motive Power HYD. Heaving Power 20 Brake Capacity 50.4 Hauling Speed 15 Metres/Min ANCHORS AND WINDLASS Windlass motive power(e.g. steam, hydraulic) HYD. Hauling power 34.2 Brake holding power Anchor type HHP TYPE Weight Page 9

11 Is spare anchor carried 1 Cable diameter 84 mm. Number of shackles port cable 12 Number of shackles starboard cable TOWING ARRANGEMENTS Is the vessel fitted with a Towing Bracket Aft? YES If Yes, state SWL 200 Is Towing chain provided YES Dimensions of Towing wire Diameter 80 mm. Length 100 Metres 14.5 WINDAGE Windage on ballast draught End-on Squaremetres Lateral 4098 Squaremetres A15 NAVIGATIONAL EQUIPMENT 15.1 Magnetic compass YES 15.2 Off Course Alarm - Magnetic compass YES 15.3 Gyro compass YES Number of Units Off Course Alarm - Gyro compass YES 15.5 Gyro (Bridge) Repeaters YES Number of Units Radar 3cm YES 15.7 Radar 10cm YES 15.8 Are radars gyro stabilised? YES 15.9 Radar plotting equipment NO ARPA YES ECDIS YES Depth sounder with recorder YES Depth sounder without recorder NO Speed/distance indicator YES Doppler log YES Docking approach Doppler YES Rudder angle indicator YES Rudder angle indicator on Each Bridge Wing YES RPM indicator YES RPM indicator on Each Bridge Wing YES Controllable pitch propeller indicator N/A Thruster(s) indicator N/A Rate of turn indicator YES Radio direction finder N/A Navtex receiver YES GPS NO DGPS YES Transit SATNAV N/A Decca navigator N/A Omega N/A Loran C N/A Weather fax YES Sextant(s) YES Signal lamp ALDIS YES Anemometer YES Engine order recorder YES VDR (Voyage Data Recorder) YES Course recorder YES Are steering motor controls and engine controls fitted on bridge wings? NO Page 10

12 15.38 Is bridge equipped with a 'Dead-Man' alarm? YES What chart outfit coverage is provided World-wide YES Limited NO If limited, - please indicate area(s) covered N/A Formal chart correction system in use NAVTOR Electronic Chart system in use YES A16 COMMUNICATIONS AND ELECTRONICS 16.2 What GMDSS areas is the vessel classed for? A1 A2 A3 A4 A1,A2 and A Transponder (SART) YES 16.4 EPIRB YES 16.5 How many VHF radios are fitted on the bridge? Is vessel fitted with VHF in the cargo control room (CCR)? YES 16.7 Is the CCR connected to the vessel's internal communication system? YES 16.8 How many intrinsically safe walkie talkies are provided for cargo handling? Is vessel fitted with an INMARSAT satellite communications system? YES Does vessel carry at least three survival craft two-way radio telephones? YES Inmarsat satellite system YES Specify system type A, B or C C kHz bridge auto alarm NO Radio telephone distress frequency watch receiver YES Emergency lifeboat transceiver NO Can vessel transmit the helicopter homing signal on 410 khz? NO Full set of Radio List publications YES Page 11

13 SECTION B CARGO SYSTEMS B1 CARGO - GENERAL INFORMATION 1.1 List products which the ship is Certified to carry Butadiene (All Isomers) Biutane (All Isomers) Butylenes (All Isomers) Commercial Propane (max. 5.0 mole% ethane in the liquid phase) Propane-Butane Mixtures Propane-Butane mixtures Propylene Transport and Carriage Conditions 1.2 Minimum allowable tank temperature -50 Deg. Celsius 1.3 Maximum Permissible tank pressure 400 mbar 1.4 List Number of grades that can be loaded/discharged simultaneously and completely segregated without risk of 2 contamination? 1.5 List the Number of grades that can be carried simultaneously and completely segregated without risk of contamination? What is the Number of Products that can be conditioned by 2 reliquefaction simultaneously? 1.7 State the number of natural segregation's (NB: Separation must be by the removal of spools or the insertion of blanks) 2 B2 CARGO TANKS 2.1 Type and materials of cargo tanks Low temperature Carbon Manganese steel 2.2 Maximum allowable relief valve setting Ref. 2.3 Bar gauge IMO Setting Bar gauge USCG Setting - Bar gauge 2.3 Safety valve set pressure, - if variable stipulate range of pilot 0.4 in harbor at seagoing valves Bar gauge 2.4 Maximum allowable vacuum Bar gauge 2.5 Maximum cargo density at 15 deg Celsius 0.61 Kg/cm2 2.6 Maximum rate of cool-down 10 Deg Cel / Hour 2.7 State any limitations regarding partially filled tanks NIL 2.8 State allowable combinations of filled and empty tanks 1. FULL-FULL-FULL-FULL 2. EMPTY-FULL-EMPTY-EMPTY 3. FULL-EMPTY-FULL-FULL 4. EMPTY-FULL-EMPTY-FULL 5. FULL-EMPTY-FULL-EMPTY Page 12

14 B3 CARGO TANK CAPACITIES Tank number / location 1 P+S Capacity m3 (100%) m3 Capacity 99% m3 n-butane capacity Butane temperature 0.0 Deg. C iso-butane capacity iso-butane temperature Deg. C Propane capacity Propane temperature Deg. C Propylene capacity Propylene temperature Deg. C Vinyl Chloride Monomer capacity NA Vinyl Chloride Monomer temperature - Deg. C Ethylene capacity NA Ethylene temperature - Deg. C Propylene Oxide capacity NA Propylene Oxide temperature - Deg. C Ammonia capacity NA Ammonia temperature - Deg. C Tank number / location 2 P+S Capacity m3 (100%) m3 Capacity 99% m3 n-butane capacity n-butane temperature 0.0 Deg. C iso-butane capacity iso-butane temperature Deg. C Propane capacity Propane temperature Deg. C Propylene capacity Propylene temperature Deg. C Vinyl Chloride Monomer capacity NA Vinyl Chloride Monomer temperature - Deg. C Ethylene capacity NA Ethylene temperature - Deg. C Propylene Oxide capacity NA Propylene Oxide temperature - Deg. C Ammonia capacity NA Ammonia temperature - Deg. C Tank number / location 3 P+S Capacity m3 (100%) m3 Capacity 99% m3 n-butane capacity n-butane temperature 0.0 Deg. C iso-butane capacity iso-butane temperature Deg. C Propane capacity Propane temperature Deg. C Propylene capacity Propylene temperature Deg. C Vinyl Chloride Monomer capacity NA Vinyl Chloride Monomer temperature - Deg. C Ethylene capacity NA Ethylene temperature - Deg. C Propylene Oxide capacity NA Propylene Oxide temperature - Deg. C Ammonia capacity NA Ammonia temperature - Deg. C Page 13

15 Tank number / location 4 P+S Capacity m3 (100%) m3 Capacity 99% m3 n-butane capacity n-butane temperature 0.0 Deg. C iso-butane capacity iso-butane temperature Deg. C Propane capacity Propane temperature Deg. C Propylene capacity Propylene temperature Deg. C Vinyl Chloride Monomer capacity NA Vinyl Chloride Monomer temperature - Deg. C Ethylene capacity NA Ethylene temperature - Deg. C Propylene Oxide capacity NA Propylene Oxide temperature - Deg. C Ammonia capacity NA Ammonia temperature - Deg. C Total Capacity of all cargo tanks (100%) m3 Total Capacity of all cargo tanks (99%) m3 Total Capacity of n-butane Total Capacity of iso-propane Total Capacity of Propane Total Capacity of Propylene Total Capacity of Vinyl Chloride Monomer NA Total Capacity of Ethylene NA Total Capacity of Propylene Oxide NA Total Capacity of Ammonia B16 DECK TANK CAPACITIES Are Deck pressure tank(s) fitted? NO Material of tank(s) N/A Maximum allowable relief valve setting - Bar gauge Page 14

16 Deck tank number 1 - capacity (100%) - m3 Capacity 98% - m3 Propane Capacity - Butane Capacity - Propylene capacity - Ethylene capacity - Ammonia Capacity - Deck tank number 2 - capacity (100%) - m3 Capacity 98% - m3 Propane Capacity - Butane Capacity - Propylene capacity - Ethylene capacity - Ammonia Capacity - B4 LOADING RATES 4.1 From Refrigerated Storage (Fully Refrigerated at Vessel's Manifold) Butane - with vapour return 2880 /Hr. Butane - without vapour return 2880 /Hr. Propane - with vapour return 2784 /Hr. Propane - without vapour return 2784 /Hr. Butadiene - with vapour return 3124 /Hr. Butadiene - without vapour return 3124 /Hr. Propylene - with vapour return 2923 /Hr. Propylene - without vapour return 2923 /Hr. Ethylene - with vapour return NA /Hr. Ethylene - without vapour return NA /Hr. Ammonia - with vapour return NA /Hr. Ammonia - without vapour return NA /Hr. Vinyl Chloride Monomer - with vapour return NA /Hr. Vinyl Chloride Monomer - without vapour return NA /Hr. Propylene Oxide - with vapour return NA /Hr. Propylene Oxide - without vapour return NA /Hr. 4.8 From Pressure Storage Butane 0 deg C - with vapour return 2880 /Hr. 0 deg C - without vapour return 2880 /Hr. 10 deg C - with vapour return - /Hr. 10 deg C - without vapour return - /Hr. 20 deg C - with vapour return - /Hr. 20 deg C - without vapour return - /Hr. Propane minus 30 deg C - with vapour return - /Hr. Minus 30 deg C - without vapour return - /Hr. Minus 20 deg C - with vapour return - /Hr. Minus 20 deg C - without vapour return - /Hr. Minus 10 deg C - with vapour return - /Hr. Minus 10 deg C - without vapour return - /Hr. 0 deg C - with vapour return - /Hr. 0 deg C - without vapour return - /Hr. 10 deg C - with vapour return - /Hr. 10 deg C - without vapour return - /Hr. 20 deg C - with vapour return - /Hr. 20 deg C - without vapour return - /Hr. Page 15

17 Butadiene 0 deg C - with vapour return - /Hr. 0 deg C - without vapour return - /Hr. 10 deg C - with vapour return - /Hr. 10 deg C - without vapour return - /Hr. 20 deg C - with vapour return - /Hr. 20 deg C - without vapour return - /Hr. Propylene minus 30 deg C - with vapour return - /Hr. Minus 30 deg C - without vapour return - /Hr. Minus 20 deg C - with vapour return - /Hr. Minus 20 deg C - without vapour return - /Hr. Minus 10 deg C - with vapour return - /Hr. Minus 10 deg C - without vapour return - /Hr. 0 deg C - with vapour return - /Hr. 0 deg C - without vapour return - /Hr. 10 deg C - with vapour return - /Hr. 10 deg C - without vapour return - /Hr. 20 deg C - with vapour return - /Hr. 20 deg C - without vapour return - /Hr. Ethylene minus 100 deg C - with vapour return NA /Hr. Minus 100 deg C - without vapour return /Hr. Minus 95 deg C - with vapour return /Hr. Minus 95 deg C - without vapour return /Hr. Minus 90 deg C - with vapour return /Hr. Minus 90 deg C - without vapour return /Hr. Minus 85 deg C - with vapour return /Hr. Minus 85 deg C - without vapour return /Hr. Ammonia minus 20 deg C - with vapour return - /Hr. Minus 20 deg C - without vapour return - /Hr. Minus 10 deg C - with vapour return - /Hr. Minus 10 deg C - without vapour return - /Hr. 0 deg C - with vapour return - /Hr. 0 deg C - without vapour return - /Hr. VCM minus 10 deg C - with vapour return NA /Hr. Minus 10 deg C - without vapour return /Hr. 0 deg C - with vapour return /Hr. 0 deg C - without vapour return /Hr. 10 deg C - with vapour return /Hr. 10 deg C - without vapour return /Hr. 20 deg C - with vapour return /Hr. 20 deg C - without vapour return /Hr Special remarks: Note 1: The figures given apply for four cargo tanks and three reliquefaction units in operation, where applicable, and for +20 degc ambient temperature. Note 2: Loading a fully refrigerated vessel from pressurized storage will give unacceptable loading times and therefore not deemed applicable for this type of vessel. B5 DISCHARGING - GENERAL Cargo Pumps 5.1 Type of Pumps Hamworthy Svanehoj DW 250/ k Number of pumps per tank Rate per Pump 600 m3/hr 5.4 At Delivery Head mlc 120 mlc 5.5 Maximum density 610 Kg/m3 Page 16

18 Booster Pump 5.6 Type of Booster Pumps Hamworthy Svanehoj NMB 150e 5.7 Number of pumps Rate per Pump 600 m3/hr 5.9 At Delivery Head mlc 115 mlc 5.10 Maximum density 690 Kg/m3 Copies of pumping curves for cargo and booster pumps are enclosed? NO B6 DISCHARGE PERFORMANCE Full Cargo Discharge Times (using all cargo pumps) Fully Refrigerated Manifold Back Press 1 kp/cm2, with vapour return 15 Manifold Back Press 1 kp/cm2, without vapour return 17 Manifold Back Press 5 kp/cm2, with vapour return 18 Manifold Back Press 5 kp/cm2, without vapour return 20 Manifold Back Press 10 kp/cm2, with vapour return 22 Manifold Back Press 10 kp/cm2, without vapour return 22 Pressurised Manifold Back Press 1 kp/cm2, with vapour return NA Manifold Back Press 1 kp/cm2, without vapour return NA Manifold Back Press 5 kp/cm2, with vapour return NA Manifold Back Press 5 kp/cm2, without vapour return NA Manifold Back Press 10 kp/cm2, with vapour return NA Manifold Back Press 10 kp/cm2, without vapour return NA B7 UNPUMPABLES 7.1 Tank number / location Tank 1, P&S: 56 mt Tank number / location Tank 2, P&S: 70 mt Tank number / location Tank 3, P&S: 70 mt Tank number / location Tank 4, P&S: 65 mt Total 261 mt B8 VAPORISING UNPUMPABLES 8.1 Process used Time to vaporise liquid unpumpables remaining after full cargo discharge of: Hot gas by cargo compressors 8.2 Butane Propane Butadiene N/A 8.5 Propylene Ethylene NA 8.7 Ammonia NA 8.8 Vinyl Chloride Monomer NA 8.9 Propylene Oxide NA B9 RELIQUEFACTION PLANT 9.1 Plant Design Conditions - air temperature 45 Deg. C 9.3 Plant Design Conditions - sea temperature 36 Deg. C Page 17

19 Plant Type 9.4 Is the plant single stage/direct? Is the plant two stage/direct? Two/Three stage 9.6 Is the plant simple cascade? Coolant type NA Compressors 9.8 Compressor type Piston Compressor makers name Buckhardt Compression 9.9 Number of compressors Capacity per unit Depending on type of cargo 9.11 Are they Oil Free? Yes B11 CARGO TEMPERATURE LOWERING CAPABILITY (AT SEA WITH SEA TEMPERATURE +15C) Time taken to lower the temperature of: 11.1 Propane from -5 deg C to - 42 deg C NA 11.2 Propane from -20 deg C to - 42 deg C NA 11.3 Propane from -38 deg C to - 42deg C Propane from +20 deg C to 0 deg C NA 11.5 Propane from 0 deg C to -20 deg C NA 11.6 Butane from +20 deg C to 0 deg C NA 11.7 Butane from +10 deg C to 0 deg C NA 11.8 Butane from +10 deg C to -5 deg C NA 11.9 Butadiene From +20 deg C to -5 deg C NA Propylene From -20 deg C to -47 deg C NA Ethylene From -100 deg C to -104 deg C NA Ammonia From -15 deg C to -33 deg C NA Vinyl Chloride Monomer From -5 deg C to -14 deg C NA B12 INERT GAS AND NITROGEN Main IG Plant 12.1 Type of system Inert Gas Generator 12.2 Capacity 5300 Nm3/hr 12.3 Type of fuel used Marine diesel oil DMA 12.4 Composition of IG - oxygen 1-2 % Composition of IG - CO2 Approx. 14 % Composition of IG - Nox Max 100 ppm Composition of IG - N2 Balance % 12.5 Lowest dewpoint achievable -40 Deg. C 12.6 Used for Inerting of cargo tanks and holds Auxiliary IG or Nitrogen plant 12.7 Type of System NA 12.8 Capacity - m3/hr 12.9 Composition of IG - oxygen - % Composition of IG - CO2 - % Composition of IG - Nox - Composition of IG - N2 - % Page 18

20 12.10 Lowest dewpoint achievable - Deg. C Used for - Nitrogen Liquid storage capacity NA m Daily boil-off loss NA m Maximum supply pressure - Kp/Cu. Cm Supply capacity - m3/hr Used for B13 CARGO TANK INERTING/DE-INERTING 13.1 Time taken to inert from fresh air to under 5% O2 at minus degree C? 13.2 Time taken to inert from cargo vapour to fully inert at minus 25 degrees dewpoint when IG density is less than product? 19 Time taken to inert from cargo vapour to fully inert at minus 25 degrees dewpoint when IG density is greater than product? NA B14 GAS FREEING TO FRESH AIR 14.1 Plant used 14.2 Time taken from fully inert condition to fully breathable fresh air? 36 Vent fans B15 CHANGING CARGO GRADES Indicate number of hours needed to change grades from the removal of pumpables to tanks fit to load and the estimated quantity of Inert Gas and or Nitrogen consumed during the operation: Inert Gas Nitrogen From Propane to Butane From Propane to Butadiene From Propane to Ethylene NA NA NA From Propane to Ammonia 105 NA - From Propane to Vinyl Chloride Monomer NA NA NA From Propane to Propylene Oxide NA NA NA From Butane to Propane From Butane to Butadiene From Butane to Ethylene NA NA NA From Butane to Ammonia NA NA NA From Butane to Vinyl Chloride Monomer NA NA NA From Butane to Propylene Oxide NA NA NA From Butadiene to Propane NA NA NA From Butadiene to Butane NA NA NA From Butadiene to Ethylene NA NA NA From Butadiene to Ammonia NA NA NA From Butadiene to Vinyl Chloride Monomer NA NA NA From Butadiene to Propylene Oxide NA NA NA From Ethylene to Propane NA NA NA From Ethylene to Butane NA NA NA From Ethylene to Butadiene NA NA NA From Ethylene to Ammonia NA NA NA From Ethylene to Vinyl Chloride Monomer NA NA NA From Ethylene to Propylene Oxide NA NA NA From Ammonia to Propane NA NA NA From Ammonia to Butane NA NA NA From Ammonia to Butadiene NA NA NA From Ammonia to Ethylene NA NA NA From Ammonia to Vinyl Chloride Monomer NA NA NA From Ammonia to Propylene Oxide NA NA NA Page 19

21 From Vinyl Chloride Monomer to Propane NA NA NA From Vinyl Chloride Monomer to Butane NA NA NA From Vinyl Chloride Monomer to Butadiene NA NA NA From Vinyl Chloride Monomer to Ammonia NA NA NA From Vinyl Chloride Monomer to Ethylene NA NA NA From Vinyl Chloride Monomer to Propylene Oxide NA NA NA From Propylene Oxide to Propane NA NA NA From Propylene Oxide to Butane NA NA NA From Propylene Oxide to Butadiene NA NA NA From Propylene Oxide to Ethylene NA NA NA From Propylene Oxide to Vinyl Chloride Monomer NA NA NA From Propylene Oxide to Ammonia NA NA NA Cargo Grade Change Operations that cannot be carried out at sea: Cargo grade change operations applicable for Propylene cannot be carried out at sea since they require Nitrogen supply from shore terminal. B17 PRE-LOADING COOLDOWN The following questions ask the Time and Quantity of coolant required to cooldown cargo tanks from ambient temperature to fully gassed up state sufficient to allow loading to commence Propane - Quantity of Coolant Required 420 t Propane - Time required to cooldown cargo tanks from 36 ambient temperature with vapour return line Propane - Time required to cooldown cargo tanks from 48 ambient temperature without vapour return line 17.2 Butane - Quantity of Coolant Required 420 t Butane - Time required to cooldown cargo tanks from 24 ambient temperature with vapour return line Butane - Time required to cooldown cargo tanks from 36 ambient temperature without vapour return line Hrs Butadiene - Quantity of Coolant Required NA m3 Butadiene - Time required to cooldown cargo tanks from NA ambient temperature with vapour return line Butadiene - Time required to cooldown cargo tanks from NA ambient temperature without vapour return line 17.4 Propylene - Quantity of Coolant Required 420 t Propylene - Time required to cooldown cargo tanks from NA ambient temperature without vapour return line Propylene - Time required to cooldown cargo tanks from 55 ambient temperature with vapour return line 17.5 Ethylene - Quantity of Coolant Required NA m3 Ethylene - Time required to cooldown cargo tanks from - ambient temperature with vapour return line Ethylene - Time required to cooldown cargo tanks from - ambient temperature without vapour return line Hrs Ammonia - Quantity of Coolant Required m3 Ammonia - Time required to cooldown cargo tanks from ambient temperature with vapour return line Ammonia - Time required to cooldown cargo tanks from ambient temperature without vapour return line Page 20

22 17.7 VCM - Quantity of Coolant Required NA m3 VCM - Time required to cooldown cargo tanks from - ambient temperature without vapour return line VCM - Time required to cooldown cargo tanks from - ambient temperature with vapour return line B18 VAPORISER 18.1 Type of Vaporiser Shell and Tube type / Seawater heater 18.2 Number of Vaporisers fitted Capacity per unit - Propane 4800 m3/hr Vap 18.4 Liquid Supply Rate 19.2 m3/hr Liq 18.5 Delivery Temperature 0 Deg. C 18.6 Capacity per unit - Ammonia NA m3/hr Vap 18.7 Liquid Supply Rate NA m3/hr Liq 18.8 Delivery Temperature NA Deg. C 18.9 Capacity per unit - Nitrogen NA m3/hr Vap Liquid Supply Rate - m3/hr Liq Delivery Temperature - Deg. C B19 BLOWER 19.1 Type of Blower 2 off Centrifugal fans 19.2 Rated Capacity 10,000 m3/hr 19.3 Delivery Pressure 0.12 Kp/cm2 B20 CARGO RE-HEATER 20.1 Type of Re-Heater Shell and Tube type 20.2 Number Fitted Heating Medium Seawater 20.4 Discharge rates with sea water at 15 degrees C to raise product temperature of Propane from -42 degrees C to degrees C m3/hr 20.5 Discharge rates with sea water at 15 degrees C to raise product temperature of Ammonia from -33 degrees C to 0 N/A degrees C m3/hr B21 HYDRATE CONTROL 21.1 Type of Depressant? Ethanol Freezing point temperature? -114 Deg. C 21.2 Quantity of Depressant Carried? 1200 Ltr Means of injection? Portable container with hand pump Name any other system used - B22 CARGO MEASUREMENT Level Gauges 22.1 Are level gauges local or remote? Remote 22.2 Name of manufacture Kongsberg Maritime 22.3 Type Radar beam type GL-100/ Rated Accuracy +/- 2 mm Certifying Authority DNV Temperature Gauges 22.6 Name of manufacture Kongsberg Maritime 22.7 Type PT Rated Accuracy +/ Deg. C 22.9 Certifying Authority DNV Page 21

23 Pressure Gauges Name of manufacture MRC Hypteck Type Pressure indicator Rated Accuracy 1 % Certifying Authority Oxygen Analyser Name of manufacture Riken Keiki Type RX What is the lowest level measurable? 0% Fixed Gas Analyser Name of manufacture Riken Keiki Type RKK-2002K Are Cargo tank calibration tables available? Yes Name of Measuring Company SGS Name of Certifying Authority DNV Calibration calculated to cm? Yes Calibration calculated to 1/2 cm? No Tables established to cm? Yes Tables established to mm? No Tables established to "other" (state what other) N/A Are trim and list corrections available? Yes Are temperature corrections available? Yes Are float gauge tape corrections available? NA B23 CARGO SAMPLING 23.1 May cargo samples be obtained from the levels; top, middle and bottom in all cargo tanks? Yes If no, - the arrangement for sampling is limited to: Vapour sample can be taken from top, middle and bottom levels. Liquid sample can only be taken via Cargo pump on the discharge line 23.2 Can samples be drawn from tank vapour outlet? Yes Can samples be drawn from manifold liquid line? No Can samples be drawn from manifold vapour line? No Can samples be drawn from pump discharge line? Yes 23.3 State sample connection type Ball valve full bore Size of sample connection 1/2" NPT (F) Page 22

24 B24 CARGO MANIFOLD Manifold arrangement diagram Stern Bow A B C D E F G H D E C F B G A H CL b a c Load W/L d a Ht above upper most continuous deck Light W/L b Distance from ship's side c Ht above load W/L d Ht above light W/L Center of manifold to bow M. Center of manifold to stern M. Dimension A - mm. Dimension B - mm. Dimension C 3375 mm. Dimension D 1125 mm. Dimension E 1125 mm. Dimension F 3375 mm. Dimension G 5625 mm. Dimension H 7875 mm. Page 23

25 Pipe Flange A - duty - Pipe Flange A - rating - bar Pipe Flange A - size - mm. Pipe Flange A raised or flat face - Pipe Flange B - duty - Pipe Flange B - rating - bar Pipe Flange B - size - mm. Pipe Flange B raised or flat face - Pipe Flange C - duty LIQUID 2 Pipe Flange C - rating 300# bar Pipe Flange C - size mm. Pipe Flange C raised or flat face Raised Pipe Flange D - duty VAPOUR 2 Pipe Flange D - rating 150# bar Pipe Flange D - size 254 mm. Pipe Flange D raised or flat face Raised Pipe Flange E - duty VAPOUR 1 Pipe Flange E - rating 150# bar Pipe Flange E - size 254 mm. Pipe Flange E raised or flat face Raised Pipe Flange F - duty LIQUID 1 Pipe Flange F - rating 300# bar Pipe Flange F - size mm. Pipe Flange F raised or flat face Raised Pipe Flange G - duty LIQUID 2A Pipe Flange G - rating 300# bar Pipe Flange G - size mm. Pipe Flange G raised or flat face Raised Pipe Flange H - duty VAPOUR 2A Pipe Flange H - rating 150# bar Pipe Flange H - size 254 mm. Pipe Flange H raised or flat face Raised Height above uppermost continuous deck 2110 mm. Distance from ship side 4250 mm. Height above load waterline mm. Height above light waterline (Ballast cond.(dep)) mm. Manifold Arrangement Located on Top of Compressor Distance from rail of compressor room/platform to presentation flanges Distance from deck of compressor room/platform/try to centre of manifold NA NA mm. mm. B25 CARGO MANIFOLD REDUCERS 25.1 Number of ANSI Class 300 reducers carried onboard 8 Flange rating of ANSI Class 300 reducer 300# bar Size of ANSI Class 300 reducer 14x16, 14x12, 14x10, 14x8 inch Length of ANSI Class 300 reducer 645 mm Number of ANSI Class 300 to Class 150 reducers carried onboard 10 Flange rating of ANSI Class 300 to Class 150 reducer 300#,150# bar Size of ANSI Class 300 to Class 150 reducer 14x16,14x14,14x12,14x10,14x8 Length of ANSI Class 300 to Class 150 reducer 645 mm Number of ANSI Class 150 reducers carried onboard 6 Flange rating of Class 150 reducer 150# bar Size of ANSI Class 150 reducer 10x12,10x8,10x6 mm. Length of ANSI Class 150 reducer 500 mm. inch Page 24

26 B26 CONNECTIONS TO SHORE FOR ESD AND COMMUNICATIONS SYSTEMS 26.1 Is ESD connection to shore available? Yes If yes, is the system pneumatic? Yes If yes, is the system electrical? Yes If yes, is the system fiber optic? What is the type of connection used? SIGGTO 26.3 Are ESD hoses or cables available on board? Yes If yes, length of pneumatic mm. If yes, length of electrical 30 meters mm. If yes, length of fiber optic - mm Is there a connection available for a telephone line? No 26.5 Are ESD connections available on both sides of vessel? Yes Are ESD Fusible plugs fitted at tank domes? Yes Are ESD Fusible plugs fitted at manifolds? Yes Is the link compatible with the SIGTTO guidelines? Yes Type of manifold valve Butterfly Closing time in seconds 27 secs Is closing time adjustable? Yes Is Independent high level shut down system fitted(overflow control)? Yes If yes, does the independent high level shutdown system also switch off running cargo pumps? Yes Shut down level % 99.5 % B27 MANIFOLD DERRICK/CRANE 27.1 Is manifold derrick provided NA 27.2 Is manifold crane provided YES 27.3 Is lifting equipment same for port and starboard? YES If no, then stipulate details THE LOCATION IS SHIP'S CENTER 27.4 State SWL at maximum outreach Maximum outreach of lifting equipment 6.7 Metres B28 STORES DERRICK/CRANE 28.1 State location PORT AND STBD AFT OF ACCOM. EL. MOTOR HANDLING SWL 5 / 5 B29 SISTER VESSEL(S) 29.1 Name of vessel BW FRIGG BW NJORD AURORA VAR AURORA FREYA AURORA BRAGE Page 25